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| United States Patent Application |
20120006486
|
| Kind Code
|
A1
|
|
CHEBI; Robert P.
;   et al.
|
January 12, 2012
|
METHOD AND APPARATUS FOR REMOVING PHOTORESIST
Abstract
A method and apparatus remove photoresist from a wafer. A process gas
containing sulfur (S), oxygen (O), and hydrogen (H) is provided, and a
plasma is generated from the process gas in a first chamber. A
radical-rich ion-poor reaction medium is flown from the first chamber to
a second chamber where the wafer is placed. The patterned photoresist
layer on the wafer is removed using the reaction medium, and then the
reaction medium flowing into the second chamber is stopped. Water vapor
may be introduced in a solvation zone provided in a passage of the
reaction medium flowing down from the plasma such that the water vapor
solvates the reaction medium to form solvated clusters of species before
the reaction medium reaches the wafer. The photoresist is removed using
the solvated reaction medium.
| Inventors: |
CHEBI; Robert P.; (San Carlos, CA)
; WINNICZEK; Jaroslaw W.; (Daly City, CA)
|
| Assignee: |
LAM RESEARCH CORPORATION
Fremont
CA
|
| Serial No.:
|
241087 |
| Series Code:
|
13
|
| Filed:
|
September 22, 2011 |
| Current U.S. Class: |
156/345.26; 156/345.29 |
| Class at Publication: |
156/345.26; 156/345.29 |
| International Class: |
C23F 1/08 20060101 C23F001/08 |
Claims
1. An apparatus for removing p
hotoresist from a wafer, the apparatus
comprising: a first chamber for generating a plasma from a process gas,
the first chamber having a gas inlet; a gas source in fluid connection
with the gas inlet, for providing the process gas containing sulfur (S),
oxygen (O), and hydrogen (H) into the first chamber; a second chamber for
placing the wafer having a patterned photoresist layer thereon; a
reaction medium distributing section for flowing a radical-rich ion-poor
reaction medium from the plasma in the first chamber to the second
chamber; and a water vapor inlet provided to the second chamber or the
reaction medium distribution section, the water vapor inlet introducing
water vapor in a solvation zone provided in a passage of the reaction
medium flowing down from the plasma to the wafer such that the water
vapor solvates the reaction medium to form solvated clusters of species
before the reaction medium reaches the wafer.
2. The apparatus according to claim 1, wherein the process gas contains
SO.sub.2, H.sub.2O and O.sub.2.
3. The apparatus according to claim 2, wherein the plasma generated from
the process gas includes HSO.sub.4. monosulfate radical, HSO.sub.3.
bisulfite radical, HO. hydroxyl radical; and O. oxygen radical.
4. The apparatus according to claim 1, wherein the process gas further
contains fluorine containing gas.
5. The apparatus according to claim 4, wherein the fluorine containing
gas contains fluorocarbon.
6. The apparatus according to claim 1, wherein the water vapor inlet
includes: a nozzle configured to inject the water vapor such that the
water vapor condenses as clusters around species of the reaction medium.
7. The apparatus according to claim 1, wherein the solvation zone is
provided in the first chamber downstream of the plasma, the reaction
medium being solvated before the reaction medium enters into the second
chamber.
8. The apparatus according to claim 1, wherein the solvation zone is
provided in the second chamber.
9. The apparatus according to claim 8, further comprising: at least one
gas distribution component having a plurality of holes, wherein the
reaction medium is transported to the wafer through the at least one gas
distribution component.
10. The apparatus according to claim 9, wherein the water vapor is
injected above the gas distribution component.
11. The apparatus according to claim 9, wherein the water vapor is
injected below the gas distribution component.
12. The apparatus according to claim 9, wherein the water vapor is
injected between two gas distribution components.
13. The apparatus according to claim 1, wherein the water vapor inlet
includes: an orifice configured to cause the water vapor to enter into
the reaction medium and condense around the species of the reaction
medium such that the species are surrounded by a number of water
molecules.
14. The apparatus according to claim 13, further comprising: a controller
configured to control: a pressure differential between a gas feed line of
the water vapor and the salvation zone where the water vapor is injected.
15. The apparatus according to claim 1, further comprising: a second gas
inlet configured to inject a fluorine containing gas in the solvation
zone.
16. The apparatus according to claim 1, further comprising: a RF power
source configured to generate the plasma; and a bias power source
configured to generate bias voltage having a frequency of 13.56 MHz and
above.
17. The apparatus according to claim 16, wherein the RF power source and
the bias power source are further configured to pulse the plasma
discharge so as to release negative ions into the reaction medium.
Description
CROSS REFERENCE TO RELATED APPLICATION
[0001] This application is a Divisional of and claims benefit of priority
to U.S. patent application Ser. No. 12/257,216 filed Oct. 23, 2008, which
is incorporated herein by reference.
BACKGROUND OF THE INVENTION
[0002] The present invention relates to the formation of semiconductor
devices. More specifically, the present invention relates to removal of
photoresist.
[0003] During semiconductor wafer processing, features of the
semiconductor device are defined in the wafer using well-known patterning
and etching processes. Photoresist (PR) is used to protect some areas of
the wafer from etch chemistries so as to define the features. Photoresist
is also used as ion implantation masks for implanting a dopant into a
silicon substrate. Conventionally, photoresist masks are removed by a
"wet" process in back end of line (BEOL) processing, for example, after
metallization, while a "dry" process is used in front end of line (FEOL)
processing, for example, after ion implantation that characterizes
devices. However, dry stripping may be used in the BEOL processing, and
wet stripping may be used in the FEOL processing. Dry photoresist strip
may be conducted either in a downstream environment or in a direct low
bias-potential plasma. In FEOL processing, active areas (Si or SiGe),
doped or undoped, are subjected to various levels of implants, followed
by photoresist strip and post strip cleans.
[0004] Effects on active area from dry or wet processes can be detrimental
from a material or dopant loss prospective. Material loss can occur as
the active area is subjected to repetitive strip-and-cleans or etch
processes. Material loss is generally defined as the conversion of active
species such as silicon or dopants to their inactive compounds such as
oxides. As material loss increases, various device characteristics, such
as drive current, leakage, resistivity, and short channel effects, also
change. Device sensitivity to material loss increases even further as
device geometries decrease 45 nm and beyond, where junctions are
shallower and more lightly doped by high-flux, low-energy ion
implantation. Active area characteristics are a precision-engineered part
of any device for optimum performance, and therefore, material loss due
to FEOL processing--such as post ion implant strip (PIIS), may be
detrimental to device performance. Furthermore, the ions implanted in the
photoresist chemically modify the near-surface regions, causing
decomposition, cross-linking, etc., of the photoresist. Such chemically
modified regions form a hard crust, where the polymer may become
graphitic in nature. Such a hard crust is typically formed in the upper
resist region and at exposed sidewalls.
[0005] In order to avoid material loss due to ion bombardment in dry strip
processes, improved wet processes with a hot sulfuric acid have also been
used. However, typical wet photoresist strip chemistries, such as hot
Piranha solutions (H2SO4:H2O2), do not work well when such crusts exist.
In order to strip such crusts, aggressive plasma strip chemistries are
being used, which typically include highly oxidizing radicals. To enhance
the crust strip, the wafer may be heated, and fluorine (F)-containing
species may be added to the plasma. However, use of such harsh chemicals
(i.e., reduction or fluorination) and/or oxidation leads to Si material
loss as well as dopants and Ge, which impacts device performance.
SUMMARY OF THE INVENTION
[0006] To achieve the foregoing and in accordance with the purpose of the
present invention, a method for removing photoresist from a wafer is
provided. The wafer has a patterned photoresist layer thereon. A process
gas containing sulfur (S), oxygen (O), and hydrogen (H) is provided, and
a plasma is generated from the process gas in a first chamber. A
radical-rich ion-poor reaction medium is flown from the first chamber to
a second chamber where the wafer is placed. The patterned photoresist
layer on the wafer is removed using the reaction medium, and then the
reaction medium flowing into the second chamber is stopped.
[0007] In another manifestation of the invention, water vapor is
introduced in a solvation zone provided in a passage of the reaction
medium flowing down from the plasma such that the water vapor solvates
the reaction medium to form solvated clusters of species before the
reaction medium reaches the wafer. The p
hotoresist is removed using the
solvated reaction medium. The solvation zone may be provided in the first
chamber downstream of the plasma, and the reaction medium is solvated
before the reaction medium enters into the second chamber. Alternatively,
the solvation zone may be provided in the second chamber.
[0008] In another manifestation of the invention, an apparatus for
removing photoresist from a wafer is provided. The apparatus includes a
first chamber for generating a plasma from a process gas, a gas source, a
second chamber, and a reaction medium distribution section. The first
chamber has a gas inlet, and the gas source is in fluid connection with
the gas inlet. The gas source provides the process gas containing sulfur
(S), oxygen (O), and hydrogen (H) into the first chamber. The wafer
having a patterned photoresist layer thereon is placed in the second
chamber. The reaction medium distributing section flows a radical-rich
ion-poor reaction medium from the plasma in the first chamber to the
second chamber. A water vapor inlet is provided to the second chamber or
the reaction medium distribution section. The water vapor inlet
introduces water vapor in a solvation zone provided in a passage of the
reaction medium flowing from the plasma to the wafer such that the water
vapor solvates the reaction medium to form solvated clusters of species
before the reaction medium reaches the wafer. The water vapor inlet may
include a nozzle which is configured to inject the water vapor so as to
condensate as clusters around the species.
[0009] These and other features of the present invention will be described
in more detail below in the detailed description of the invention and in
conjunction with the following figures.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010] The present invention is illustrated by way of example, and not by
way of limitation, in the figures of the accompanying drawings and in
which like reference numerals refer to similar elements and in which:
[0011] FIGS. 1A and 1B are schematic cross-sectional views of examples of
a substrate having a photoresist mask for ion implantation.
[0012] FIG. 2 is a high level flow chart of a process that may be used in
an embodiment of the invention.
[0013] FIG. 3 is a schematic cross-sectional view of a plasma processing
module which may be used for performing the photoresist removal in
accordance with one embodiment of the present invention.
[0014] FIGS. 4A and 4B schematically illustrate examples of a downstream,
inductively coupled plasma processing module which may be used for
performing photoresist removal in accordance with another embodiment of
the present invention.
[0015] FIG. 5 schematically illustrates another example of a downstream,
inductively coupled plasma processing module which may be used for
performing photoresist removal in accordance with yet another embodiment
of the present invention.
[0016] FIG. 6 schematically illustrates a downstream p
hotoresist stripping
chamber ("downstream chamber") which may be used for performing
photoresist removal in accordance with yet another embodiment of the
present invention.
[0017] FIGS. 7A-7C schematically illustrate other examples of a plasma
module (stripper module) having temperature control which may be used for
performing p
hotoresist removal in accordance with one embodiment of the
present invention.
[0018] FIG. 8 is a flow chart of the solvation process of the reaction
medium being transported from the plasma to the wafer in accordance with
one embodiment of the present invention.
[0019] FIG. 9 schematically illustrates an example of the plasma
processing module having an additional water vapor inlet in accordance
with one embodiment of the present invention.
[0020] FIG. 10 schematically illustrates another example of the plasma
processing module in which the injection port is used as an additional
water vapor inlet in accordance with one embodiment of the present
invention.
[0021] FIGS. 11A-12 schematically illustrates other examples of plasma
processing modules having a water vapor inlet in accordance with
embodiments of the present invention.
[0022] FIG. 13 schematically illustrates an example in which the second
chamber of the plasma module includes more than one baffles (gas
distribution components).
[0023] FIGS. 14A-14B schematically illustrate other examples of a plasma
processing module in which an additional gas injection port is used as a
water vapor inlet, in accordance with embodiments of the present
invention.
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0024] The present invention will now be described in detail with
reference to a few preferred embodiments thereof as illustrated in the
accompanying drawings. In the following description, numerous specific
details are set forth in order to provide a thorough understanding of the
present invention. It will be apparent, however, to one skilled in the
art, that the present invention may be practiced without some or all of
these specific details. In other instances, well known process steps
and/or structures have not been described in detail in order to not
unnecessarily obscure the present invention.
[0025] FIGS. 1A and 1B schematically illustrate a cross-sectional view of
examples of a substrate 10 having a photoresist mask 12 for ion
implantation. The substrate 10 may also include a thin dielectric layer
14. The photoresist mask 12 has features which define active areas 16
where dopants are injected, as shown in FIG. 1A. The photoresist mask 12
may also be used, as shown in FIG. 1B, for example, to protect a p-type
device area 18 when active areas 20 for an n-type device are formed by
ion implantation. After the ion implantation, the near-surface regions of
the photoresist mask are chemically modified by ion injection, forming a
hard crust 22 covering a bulk portion 24.
[0026] In general, downstream photoresist stripping is performed by
discharging oxygen with fluorocarbon addition in a microwave or RF
discharge zone. The radicals from the plasma are transported to a process
chamber, where ions are typically left behind. In order to facilitate an
acceptable reaction rate, the wafer may be heated up to 300.degree. C.
Material loss during downstream strip occurs by diffusion of radicals
(O*) into silicon, which convert the silicon into silicon dioxide, where
the high temperature increases the diffusion. Alternatively, if the
direct low bias-potential plasma strip is used, material loss occurs due
to charged chemical species (O+ or O2+) from the plasma penetrating
through the thin dielectric layer into the active area.
[0027] In both types of dry strip the radials or ions react with the Si,
Ge, or dopants, and basically incapacitate them. An example for such
chemical species can be oxidizing radicals that are driven through the
thin dielectric layer by sufficient thermal energy to react with or
consume active area constituents. The active area constituents are
oxidized or even removed during dry strip. Results of such an action lead
to the loss of active area Si or Ge. Reducing species (i.e., hydrogen)
can be equally as disruptive to cause material loss in the active areas,
although this is not through oxidation. In addition, as an alternative to
dry photoresist removal, wet processes have been developed using aqueous
solutions of sulfuric acid and peroxide, for example, chemistry known as
SHARK, purportedly causing minimum silicon loss. However, the technology
is under development and does not work well when photoresist is hardened
or a hard crust is formed when implanted at higher doses, as described
above.
[0028] Thus, in FEOL post ion implant strip processing, Applicants have
studied and developed processes for removing a hardened photoresist (PR)
layer and the remaining bulk photoresist, without adversely affecting (or
removing) any exposed dielectric layer over the underlying active area
Silicon, which may or may not include N or P dopants and/or Ge. In
addition to stringent material loss goals, it is required that the strip
process not result in making a residue layer hard.
[0029] Embodiments of the present invention utilize a downstream plasma
module having a plasma discharge section upstream of a reaction chamber.
Embodiments of the invention use a novel process gas containing sulfur
(S), oxygen (O), and hydrogen (H).
[0030] To facilitate understanding, FIG. 2 is a high level flow chart of a
process that may be used to remove photoresist from a substrate in
accordance with an embodiment of the present invention. The wafer has a
patterned photoresist thereon. The photoresist may be used as an ion
implantation mask prior to the p
hotoresist removal, and may have a bulk
portion and a crust portion covering the bulk portion, for example, as
shown in FIG. 1A or 1B. However, it should be noted that the present
invention is also applicable to other photoresist removal, for example,
photoresist strip in the BEOL processes. Referring back to FIG. 2, a
process gas containing sulfur (S), oxygen (O), and hydrogen (H) is
provided (step 202). For example, the process gas may contain SO2, H2O
and O2. The process gas may further contain fluorine containing gas, for
example, NF6, NF3, or fluorocarbon, for example, CF4. More generally,
fluorocarbon may be expressed as CxFy (x.gtoreq.1, y.gtoreq.1) and/or
CxFyHz (x.gtoreq.1, y.gtoreq.1, z.gtoreq.1). The source gas may further
contain other component gases such as H2 and NH3.
[0031] A plasma is generated from the process gas in a first chamber (step
204). The plasma may be discharged using a microwave, an inductive
discharge (RF energy), DC discharge, or some other high density
dissociative remote source. A radical-rich ion-poor reaction medium is
flown from the first chamber to a second chamber where the wafer is
placed (step 206). The wafer has a patterned photoresist layer thereon.
The patterned photoresist layer is removed using the reaction medium
(step 208). Then, the flow of the reaction medium into the second chamber
is stopped (step 210). Additional cleaning process(es) may be performed
after the photoresist removal using the reaction medium (step 212).
[0032] FIG. 3 is a schematic cross-sectional view of a plasma processing
module 100 including a plasma chamber 102 which may be used for
performing the photoresist removal in accordance with one embodiment of
the present invention. The plasma chamber 102 includes chamber walls 104
and a dielectric window 106. The plasma processing module 100 includes a
feed gas inlet 108 for allowing feed gases to flow into the chamber 102.
An exhaust port 110 exhausts gases from the chamber 102. An inductive
source 112, typically taking the form of a coil positioned on the
dielectric window 106, is used to energize the feed gases within the
chamber 102 and ignite a plasma within the chamber 102. In this example,
the inductive source 112 is powered by an RF power supply 114.
[0033] The inductive source 112 causes the plasma within the chamber 102
to form a plasma having a primary dissociation zone 116. This primary
dissociation 116 zone is the region within the chamber 102 that the
plasma most efficiently dissociates the feed gases. In the case where the
inductive source 112 takes the form of a coil attached to the dielectric
window 106, the primary dissociation zone 116 takes the form of a
generally donut shaped region located within the chamber 102 directly
below the coils of the inductive source 112.
[0034] The plasma processing module 100 may also include a liner 118, such
as a quartz liner, or any other available material, for protecting the
walls of the plasma chamber from the plasma and reducing the
recombination of neutral radicals like O or OH. A chuck 120 is positioned
in the bottom of the chamber 102 and is configured to support a
semiconductor substrate 122. As is known in the art, the chuck 120 may be
heated to improve the efficiency of the process. The plasma processing
module 100 also includes a quartz baffle 124 located above the substrate
122. The baffle 124 includes a plurality of openings formed through the
baffle 124 which cause any gases flowing through the chamber 102 to be
redistributed so that the gases flow more evenly over the substrate 122
than would be the case if the baffle 124 were not included in the plasma
processing module 100. The baffle 124 partially shields the substrate 122
from direct exposure to the plasma. Thus, in this example, the plasma
chamber 102 above the baffle 124 is considered as a first chamber, and a
region below the baffle 124 where the substrate 122 is place on the chuck
120 is considered as a second chamber.
[0035] In accordance with one embodiment of the present invention, a novel
gas combination containing sulfur (S), oxygen (O), and hydrogen (H), for
example, a process gas containing feed gases: SO2, H2O and O2 is
introduced via the feed gas inlet 108. One of the objectives of using H2O
is to passivate active area silicon by "sealing" dangling Si bonds. The
other objective is to generate relatively large (in contrast to the
oxygen radical) powerful reagents which can attack the carbon within
photoresist, but cannot readily diffuse into active area silicon. An
optional fluorine containing gas may also be introduced into the
discharge (dissociation zone 116) in the plasma chamber 102 via the feed
gas inlet 108.
[0036] The process gas is dissociated in the primary dissociation zone 116
so as to form a radical-rich ion-poor reaction medium. In this
specification and claims, "radical-rich ion-poor" means that the radical
concentration (radicals/cm3) is greater than the ion density (ions/cm3)
at least by the factor of E2 (102), preferably by the factor E5 (105) or
greater, more preferably by the factor of E5 (105) to E8 (108), depending
on the pressure, dissociation efficiency, and recombination rate. For
example, the ion densities provided for the radical-rich ion-poor medium
may be less than 10E7 (10.times.107) ions/cm3, preferably less than 10E6
(10.times.106) ions/cm3, while the range of radical concentrations may be
5E13 (5.times.1013) to 5E15 (5.times.1015) radicals/cm3, preferably 1E14
(1.times.1014) to 1E15 (1.times.1015) radicals/cm3. However, when the
bias is applied, as described below, the ion density may be in the range
of about 10E9 (10.times.109) to 10E10 (10.times.1010) ions/cm3. The
radical-rich ion-poor reaction medium also includes a reaction medium in
which substantially no ions are present. There are many reactions with
the discharge products which will form a variety of strongly reactive
species. Some of these compounds are strong reducing agents, some are
very strong hydrogen donors, while others are oxidizing agents. By
controlling the reactive mix it is possible to balance oxidation and
reduction at the active area while effectively decomposing the
photoresist. A plasma with SO2, H2O and O2 as feed gases will generate
radicals: HSO4. monosulfate radical with properties of sulfuric acid,
HSO3. bisulfite radical, HO. hydroxyl radical; and O. oxygen radical. The
HSO4. and HSO3. radicals are strong hydrogen donors such that it can
hydrogenate the carbon in the photoresist. Additionally the HSO4. radical
is a strong oxidizing compound such that it along with HO. and O. oxidize
the weakened carbon. It should be noted that SO2, not other oxides of
sulfur, needs to be present with H2O in order to facilitate the
appropriate reaction.
HSO4.+C--C .fwdarw.H--C--C+SO4..fwdarw.CO2+OH+SO
HSO3.+O--Si--Si.fwdarw.H--Si--Si+SO4.
[0037] The radical-rich ion-poor reaction medium is flown from the primary
dissociation zone 116 of the plasma chamber 102 through the baffle 124 to
the reaction zone 126 where the substrate 122 is placed, as shown in FIG.
3. Since the baffle 124 partially shields ions from reaching the
substrate, the reaction zone 126 can be considered as a second chamber in
this example. The patterned photoresist layer on the substrate 122 is
removed using the reaction medium.
[0038] FIG. 4A schematically illustrates a downstream, inductively coupled
plasma processing module 140 which may be used for performing photoresist
removal, in accordance with another embodiment of the present invention.
For illustrative purposes, like reference numerals will be used
throughout the various figures for like components such that those of
ordinary skill in the art understand the similar components and functions
thereof without additional explanation.
[0039] Generally, the plasma processing module 140 is similar to the
plasma processing module 100 described above, except that the plasma
chamber 102 is divided into a first (upper) chamber 142 for plasma
generation and dissociation, and a second (lower) chamber 144 for
processing (photoresist removal), by a plasma containment plate 146, as
shown in FIG. 4A.
[0040] Similarly to the plasma processing module 100, the plasma
processing module 140 includes feed gas inlet 108 for allowing feed gases
to flow into the first chamber 142. Exhaust ports 110 exhausts gases from
the second chamber 144. Inductive source 112, in this case taking the
form of a coil positioned above the dielectric window 106, is used to
energize feed gases within the first chamber 142 and generate a plasma
within the first chamber 142 from the feed gases. In this example, the
inductive source 112 is powered by RF power supply 114 which takes the
form of a transformer coupled source. Typical inductive source power
ranges from about 250 W to about 5000 W or more. Similarly to the
previous embodiment, the specific configuration and shape of inductive
source 112 causes a plasma having primary dissociation zone 116 in the
first chamber 142. During plasma processing, the gas pressure within the
first chamber 142 and the second chamber 144 may be from about 10 mT to
about 10 T or more, but typically the operating pressure is about 1 T.
The feed gas flow may range from about 100 standard cubic centimeters per
minute (sccm) to about 10,000 sccm or more for a 300 mm substrate
(wafer).
[0041] An internal port 148 that interconnects the first chamber 142 and
the second chamber 144 is provided substantially at the center of the
plasma containing plate 146. The internal port 148 allows the reaction
medium generated in the first chamber 142 to flow into the second chamber
144 during the processing of the substrate 122. The second chamber 144
may have a baffle 124. The reaction zone (not shown in FIG. 4) below the
baffle 124 may be considered as part of the second chamber, or
alternatively, a third chamber.
[0042] As shown in FIG. 4A, the feed gas inlet 108 may be located such
that the flow of any feed gases fed into the first chamber 142 is
directed substantially through the primary dissociation zone 116 toward
the internal port 148 as indicated by the arrows. The plasma generated in
the first chamber 142 produces a reaction medium from the feed gases, and
the reaction medium is transported from the first chamber to the second
chamber via the internal port 148. In this embodiment, the feed gases may
be SO2, H2O and O2 which are introduced via the gas feed inlet 108. The
optional fluorine containing gas may also be provided through the gas
feed inlet 108.
[0043] Additionally, the chamber walls 104 and the plasma confinement
plate 146 may be grounded. This grounding of the walls attracts any
charged species causing them to collide with the walls thereby helping to
prevent the charged species (ions) from flowing from the first chamber
142 into the second chamber 144.
[0044] The reaction medium introduced into the second chamber 144 is thus
further radical-rich ion-poor, and preferably in accordance with an
embodiment of the present invention, the reaction medium contains
substantially no ions or charged particles.
[0045] As shown in FIG. 4A, the second chamber 144 has a quartz baffle 124
located above the substrate 122. The baffle 124 includes openings formed
through baffle 124 which cause the reaction medium flowing through the
second chamber 144 to be redistributed more evenly over the substrate 122
than would be the case without the baffle 124.
[0046] In accordance with another embodiment of the present invention,
some feed gases are injected into the plasma discharge (dissociation zone
116), while other gases may be injected downstream of the discharge. FIG.
4B schematically illustrates another example of plasma processing module
160 similar to the plasma processing module 140, in which configuration
of the feed gas inlet 108 and the internal port 148 is different, and an
additional injection port 150 is provided to the second chamber 144. In
this example, the feed gas inlet 108 is provided at substantially the
center of the top of the first chamber 142, and the internal port 148 is
provided at the both sides (or periphery) of the plasma containment plate
146. The additional injection port 150 is provided on the top wall of the
second chamber 144. In this example, all of the feed gases may be
provided through the feed gas inlet 108. Alternatively, the fluorine
containing gas may be introduced downstream of the plasma into the second
chamber 144 via the additional injection port 150. Other features are
similar to those of the plasma processing module 140 described above.
[0047] FIG. 5 schematically illustrates another example of a downstream,
inductively coupled plasma processing module 180 which may be used for
performing photoresist removal, in accordance with another embodiment of
the present invention. For illustrative purposes, like reference numerals
will be used throughout the various figures for like components such that
those of ordinary skill in the art understand the similar components and
functions thereof without additional explanation.
[0048] Generally, the plasma processing module 180 is similar to the
plasma processing modules 140 and 160 described above, except that the
internal port 148 extends downward from an upper part of the first
chamber 142 to the second chamber 144 so as to have an opening on the top
wall of the second chamber 144.
[0049] As shown in FIG. 5, the feed gas inlet 108 and the internal port
148 are provided to the first chamber 142 such that the flow of any feed
gases fed into the first chamber 142 passes substantially through the
primary dissociation zone 116 to the internal port 148. For example, the
opening of the gas feed inlet 108 and the exit to the internal port 148
may be located on the opposite side of the first chamber 142 across the
primary dissociation zone 116. Furthermore, as shown in FIG. 5, the
plasma processing module 180 further includes an injection port 150
connected to the passageway of the internal port 148 between an exit from
the first chamber 142 and an opening to the second chamber 144.
[0050] The plasma generated in the first chamber 142 produces a reaction
medium from the feed gases, and the reaction medium is transported from
the first chamber 142 to the second chamber 144 via the internal port
148. In this embodiment, the feed gases may be SO2, H2O and O2 which are
introduced via the gas feed inlet 108. The optional fluorine containing
gas or gases may be provided downstream by introducing through the
injection port 150 into the reaction medium which is being transported
from the first chamber 142 to the second chamber 144. It should be noted
that the injection port 150 may also be used to inject water vapor for
salvation as described below with respect to other embodiments of the
present invention.
[0051] Additionally, the chamber walls 104 and the plasma confinement
plate 146 which also constitute walls of the internal port 148 may be
grounded. This grounding of the walls attracts any charged species
causing them to collide with the walls thereby helping to prevent the
charged species (ions) from flowing from the first chamber 142 into the
second chamber 144.
[0052] The present invention can also be performed using a microwave
powered downstream plasma process chamber. FIG. 6 schematically
illustrates a downstream photoresist stripping chamber ("downstream
chamber") 300 in accordance with one embodiment of the present invention.
The downstream chamber 300 includes chamber walls 302, a chamber bottom
304, and a chamber top 306, which define a chamber internal region 308. A
semiconductor wafer support structure (or "chuck") 310 is positioned
within the chamber internal region 308 near the chamber bottom 304. The
chuck 310 may contain a number of lifting pins 312 that are used to raise
and lower a semiconductor wafer (or "wafer") 314 placed on the chuck 310
for processing. The chuck 310 may also include a heater 316 configured to
operate using electric power. The downstream chamber 300 also includes
exhaust system (not shown).
[0053] The downstream chamber 300 further includes an applicator tube 320
positioned above the chamber top 306. The applicator tube 320 is
configured to be in open communication with the chamber internal region
308 via a shower head 322. A processing gas supply line 324 is in fluid
communication with the applicator tube 320 to supply a processing gas.
The purpose of the applicator tube 320 is to couple microwave energy to
the feed gas and to deliver the dissociated reactive gas mixture to the
processing chamber 300. The shape of the applicator tube 320 is not
limited to that illustrated in FIG. 6, and the applicator tube may have a
different shape such as an elongate tube with an opening at the end. In
the embodiment of the present invention, the preferred processing gas
contains sulfur (S), oxygen (O), and hydrogen (H). For example, the
process gas contains SO2, H2O and O2 as feed gases. The process gas may
further contain fluorine containing gas, for example, NF6, NF3, or
fluorocarbon, for example, CF4. More generally, fluorocarbon may be
expressed as CxFy (x.gtoreq.1, y.gtoreq.1) and/or CxFyHz (x.gtoreq.1,
y.gtoreq.1, z.gtoreq.1). However, the processing gas supply line 324 can
be configured to supply virtually any type of processing gas.
[0054] A microwave power supply 326 is also connected to the applicator
tube 320 to supply microwave power to the processing gas within the
applicator tube 320. The microwave power generates a plasma and
transforms the processing gas into a reaction medium containing radicals
as its constituent elements. Thus, the applicator tube 320 functions as a
first chamber for generating the reaction medium via plasma. In
accordance with one embodiment of the present invention, a plasma with
SO2, H2O and O2 feed gases will generate radicals: HSO4. monosulfate
radical with properties of sulfuric acid, HSO3. bislufite radical, HO.
hydroxyl radical; and O. oxygen radical. The radicals include primarily H
radicals and O radicals. The radicals flow through the shower head 322
into the chamber internal region 308 toward the wafer 314. The radicals
isotropically (i.e., uniformly in direction) contact the wafer 314 and
react to remove materials present on the surface of the wafer 314. The
HSO4. and HSO3. radicals are strong hydrogen donors such that it can
hydrogenate the carbon in the photoresist. Additionally the HSO4. radical
is a strong oxidizing compound such that it along with HO. and O. oxidize
the weakened carbon.
[0055] FIG. 7A schematically illustrates another example of a plasma
module (stripper module) 400 having temperature control in accordance
with one embodiment of the present invention. The stripper module 400
includes a plasma source (with a plasma chamber) 402 and a process
chamber 408. The plasma source 402 energizes a process gas 404 into
plasma 406, for example, using a microwave or RF-powered source. The
process chamber 408 includes a chamber top 410 having a central opening,
a gas distribution component 412 secured to the chamber top 410 at the
central opening, an internal chamber body 414, a temperature controlled
chuck 420 for supporting a substrate (wafer) 422 thereon, and an external
chamber body 416 that slidably mounts the internal chamber body 414
thereon and surrounds the side of the internal chamber body 414. The
stripper module 400 also includes an exhaust unit 450 coupled thereto.
The exhaust unit 450 may include an isolation valve 452 and a throttle
valve 454 coupled to a vacuum pump 456. The plasma module 400 may also
include one or more heaters 424 and fluid cooling channels 426.
[0056] The inlet of the central opening of the chamber top 410 is aligned
with the outlet of the plasma source 402. The gas distribution component
412 has a plurality of gas passages 442 formed therein, which are
configured such that the gas exiting from the gas passages is dispersed
and uniformly fanned out. The outlet of the central opening is in fluid
communication with the inlets of the gas passages 442. The internal
chamber body 414 is positioned beneath the gas distribution component 412
and includes an upper chamber dome that has a streamlined inner surface
to reduce flow recirculation and turbulence and including a side portion
that surrounds the substrate 422 and chuck (support) 420 in the
circumferential direction of the chuck 420. However, the present
invention is not limited to those specific configurations of the chamber.
[0057] A plasma is generated in the plasma source (chamber) 402 from the
process gas containing sulfur (S), oxygen (O), and hydrogen (H), for
example, a process gas containing feed gases of SO2, H2O and O2, and an
optional fluorine containing gas. A radical-rich ion-poor reaction medium
flows downstream from the plasma 406 into the internal chamber body 414
of the process chamber 408 through the central opening and the gas
distribution component 412.
[0058] In addition, an additional gas injection port 440a may be provided,
for example, through a gap 432 between the internal chamber body 414 and
the chamber top 410, as shown in FIG. 7B. In this case, the optional
fluorine containing gas may be introduced through the gas injection port
440a into the internal chamber body downstream the gas passages from the
gas distribution component 412. Alternatively, as shown in FIG. 7C the
additional gas injection port 440b may be provided downstream the plasma
source 402 at the conical section above the gas distribution component
412, so as to inject the additional gas containing fluorine.
[0059] In accordance with one embodiment of the present invention, the
method for removing the photoresist further includes solvating the
reaction medium before reaching the plasma. To facilitate understanding,
FIG. 8 is a flow chart of the solvation process of the reaction medium
being transported from the plasma to the wafer (during the step 206 in
FIG. 2). As shown in FIG. 8, water vapor is introduced in an injection or
solvation zone that is provided in a passage of the reaction medium
flowing down from the plasma or the plasma source toward the wafer (step
220). The water is forced through a nozzle or orifice to ensure mild
condensation as clusters around ions or radicals.
[0060] The water vapor solvates the reaction medium to form solvated
clusters of species (step 222) before the reaction medium reaches the
wafer. The means to achieve clustering (or solvation) is by injecting the
water vapor through a fine orifice such that small amount of condensation
occurs. This would be condensation around the specific molecule or ion.
This downstream injection is operated such that the water vapor entering
into the flowing reaction medium (discharge stream) is allowed to
condense around species of the reaction medium generated in the plasma to
form solvated clusters. These solvated clusters include either an active
radical or ion surrounded by a number of water molecules. The number of
the water molecules may range from 3 to roughly 20, more generally, 2 to
100.
[0061] In this specification and claims, when the radicals are solvated,
it means that clusters of water molecules are formed around active
radicals, and the zone where the water vapor is injected and the radicals
are solvated is referred to as a solvation zone. As the radicals are
transported to the wafer, the reaction on the surface of the p
hotoresist
is microscopically aqueous. The formation of the clusters depends on the
pressure differential between the gas feed line and the injection zone,
as well as on the orifice size. The radicals are solvated as:
HSO4.+nH2O.fwdarw.{(SO4.)(H2O)n}
The number n may be in the range of 2 to 100 when the mild condensation
occurs.
[0062] If the number of solvating water molecules is large enough, a
single neutrally charged cluster can deliver both positive and negative
ions:
H2SO4+nH2O.fwdarw.{(SO42-)(H3O)+2 (H2O)n-2}
[0063] In accordance with one embodiment of the present invention, the
solvation zone is provided in the first chamber downstream of the plasma
such that the reaction medium is solvated before the reaction medium
enters into the second chamber. For example, as shown in FIG. 9, an
additional water vapor inlet 130 may be provided to the plasma processing
module 100 (FIG. 3) so as to inject water vapor. The reaction medium is
solvated in a solvation zone 132. The solvation zone in this embodiment
is in close proximity to the plasma generation zone. This ensures maximum
interaction of the water with the plasma. It should be noted that if the
solvation zone is too close to the plasma, it may result in dissociation
of water molecules and breaking of the clusters, and thus the proximity
should be well controlled.
[0064] In accordance with another embodiment of the present invention, the
solvation zone is provided in a passage of the reaction medium between
the first chamber and the second chamber. For example, as shown in FIG.
10, the injection port 150 in the plasma processing module 180 (FIG. 5)
can be used as an additional water vapor inlet 130 to inject water vapor.
The reaction medium is solvated in the internal port 148. The solvation
process may continue while the reaction medium is transported into the
second chamber 144. The solvation zone is removed from the plasma
generation zone to prevent the water vapor from being dissociated and
prevent the clusters from breaking up.
[0065] In accordance with yet another embodiment of the present invention,
the solvation zone is provided in the second chamber such that the
reaction medium is solvated before the reaction medium reaches the wafer.
For example, as shown in FIG. 11A, an additional water vapor inlet 130
may be provided to the plasma processing module 140 (FIG. 4A) so as to
inject water vapor. Alternatively, as shown in FIG. 11B, the additional
injection port 150 in the plasma processing module 160 (FIG. 4B), can be
used as an additional water vapor inlet 130 to inject water vapor. In
addition, as shown in FIG. 12, an additional water inlet 130 may be
provided to a downstream chamber 300 (FIG. 6) so as to provide a
solvation zone 132. The reaction medium is solvated in the solvation zone
132 in each of these examples. These configurations place the solvation
zone further down stream from the plasma source ensuring complete
clustering without interference from the plasma, since the plasma may
breakup the clusters and even dissociate the water if the solvation zone
is too close to the plasma.
[0066] FIG. 13 schematically illustrates an example in which the second
chamber 144 of the plasma module 500 includes more than one baffles (gas
distribution components). The additional water vapor inlet may be
provided either above the upper baffle 124a (water vapor inlet 130a),
between two baffles 124a and 124b (water vapor inlet 130b), or below the
lower baffle 124b (water vapor inlet 130c).
[0067] In addition, in the plasma processing module 400a (FIG. 7B) or 400b
(FIG. 7C), the additional gas injection port 440a or 440b can be used as
a water vapor inlet 430a or 430b so as to introduce water vapor to
solvate the reaction medium, as shown in FIG. 14A and 14B. As discussed
above, the water vapor inlet 430a may be provided through a gap 432
between the internal chamber body 414 and the chamber top 410 so as to
have an opening in the internal chamber body 414. In this case, the
reaction medium is solvated in the internal chamber body (the second
chamber) 414 in the solvation zone 132. Alternatively, the additional
water vapor inlet 430b may be provided downstream the plasma 406 at the
conical section above the gas distribution component 412. In this case,
the reaction medium is solvated in the solvation zone 132 (the conical
section) before entering into the internal chamber body 414 through the
gas distribution component 412. The solvation zone in FIG. 14A ensures
that predominantly radicals will be solvated since the gas distribution
component 412 will reduce (or possibly eliminate) ion flux. In contrast
the configuration of FIG. 14B ensures that a larger fraction of ions are
solvated at the expense of dissociating the water vapor or breaking the
clusters. The gas distribution component 412 is configured to maximize
ion pass through. In other words, the distribution holes in 412 are large
enough to ensure ion passage.
[0068] Furthermore, in accordance with one embodiment of the present
invention, a distance between the plasma 406 and the solvation zone 132
can be adjusted. For example, in the plasma process module 400a (FIG.
14A) or 400b (FIG. 14B), the conical section and plasma source 402 may be
raised or lowered with respect to the water vapor inlet 430a or 430b.
[0069] In accordance with another embodiment of the present invention,
ions from the plasma may be permitted to be present in the reaction
medium to reach the wafer. The objective is to force negative ions from
the plasma into the solvation zone and form negative ion clusters. Since
negative ions do not escape a plasma and congregate in the middle of the
plasma, the plasma needs to be shut off in order to get the negative ions
out. This is accomplished by pulsing the plasma on and off. That is, the
microwave or RF power to the applicator 402 is pulsed, and if there is a
bias power then that power would also be pulsed. Typical off times may be
5 to 50 microseconds, and typical on times may be 5 to 200 microseconds.
Negative ion production is best under lower pressures. The negative ions
are solvated and transported to the wafer. Negative ions are very
reactive oxidizing agents, in that they have an additional electron over
the corresponding radical.
SO42--+nH2O.fwdarw.{(SO4)(H2O)n}2-{(SO4)(H2O)n}2-+C--C.fwdarw.{CO2(H2O)1-
}+{SO2(H2O)m}
[0070] This may be achieved by making the exit holes to the second chamber
large enough. For example, in FIGS. 14A-14B, the gas distribution
component 412 may have a plurality of gas passages 442 having larger
holes such that ions pass from the plasma discharge zone 406 through the
larger holes into the internal chamber body (the second chamber) 414. The
same applies, for example, to the process module 100 (FIG. 9), the
openings of the baffle 124 may be enlarged. In the process module 140
(FIG. 11A), the process module 160 (FIG. 11B), and the process module 180
(FIG. 10), the opening of the inner port 148 interconnecting the first
chamber 142 and the second chamber 144 (or reaction chamber) can be made
larger enough such that more ions will pass through. Similarly, in
downstream chamber 300 (FIG. 12), the holes of the showerhead 322 can be
made larger.
[0071] In addition, if the process module includes an RF power source for
the lower electrode (chuck), for example, the process modules 160 or 180,
a bias voltage can be provided so as to attract the charged species
(ions) toward the wafer. The bias voltage may have a frequency of 13.56
MHz and above, for example, 27 MHz. In these cases, the holes of the
baffles can also be enlarged. Furthermore, the top RF power source to
generate plasma may be pulsed to release negative ions. In general, a
continuous plasma has a sheath which prevents relatively bulky negative
ions from getting past the sheath boundary. As the plasma is turned off,
the sheath collapses and the negative ions are released. The quartz
baffle(s) may be biased such that the negative ions will pass through the
quartz baffle, for example, in the process module 100 (FIG. 10).
[0072] In addition to negative ions, positive ions will also be
transported. Ions such as H+ and H3O+ are strong reducing agents. The
combination of oxidation with negative ions and reduction with positive
ions will effectively breakdown the photoresist while checking excessive
oxidation or reduction of the active area silicon.
[0073] In all of those embodiments of this invention, the addition of
fluorocarbons is employed to assist in the breakthrough of implant
generated crust. The fluoride radical and negative ions are very strong
oxidizers for breaking through cross-linked carbon bonds.
[0074] In accordance with another embodiment of the present invention, the
timing/sequence of introducing the process gas(es) and the water vapor
may be changed in order to control effects on the photoresist strip
process, such as the strip rate, strip residue, amount of material loss,
or other on-wafer results in general. When a wafer is placed in the
second chamber separate from the first chamber where the plasma is
generated, the timing of introducing the process gases into the first
chamber also controls the timing of the reaction medium to flow into the
second chamber with respect to the water vapor injection.
[0075] According to a first example, the process gas(es) and the water
vapor may be introduced/injected into the respective locations in the
chamber(s) at the same time. In a second example, the water vapor is
first injected, followed by the process gases after a certain time delay.
This may have different surface kinetics, and may enhance absorption.
Alternatively, the process gases are introduced first, followed by
injection of water vapor after a certain time delay. This sequence also
has different surface kinetics. In accordance with a forth example, water
vapor is first injected, then only the process gasses are introduced
(i.e., the water vapor injection is being stopped during the introduction
of the process gasses), followed by water vapor injection without
introducing the process gases, followed by the process gases introduction
without water vapor injection, and so forth. The forth example is an
alternating process in which the water vapor and the process gases are
introduced in an alternating and sequential manner. This may enhance
surface absorption and reaction. The sequence ("water first" or "process
gas first") and the time duration of each injection/introduction step may
also be controlled to optimize the surface results.
[0076] In accordance with another embodiment of the present invention, a
diluent gas may be added to the process gas chemistry in any of the
embodiments described above.
[0077] While this invention has been described in terms of several
preferred embodiments, there are alterations, permutations, and various
substitute equivalents, which fall within the scope of this invention. It
should also be noted that there are many alternative ways of implementing
the methods and apparatuses of the present invention. It is therefore
intended that the following appended claims be interpreted as including
all such alterations, permutations, and various substitute equivalents as
fall within the true spirit and scope of the present invention.
* * * * *